Sulfonated perfluoroelastomer composition having improved processability

ABSTRACT

Curable perfluoroelastomer compositions are prepared in the presence of an initiator system comprising a mixture of a persulfate salt and a reducing agent wherein the amount of reducing agent present is no more than 20 mole percent of the total initiator system. The perfluoroelastomer is isolated and decarboxylated, thereby providing a product having excellent processability.

CLAIM OF BENEFIT OF PRIOR APPLICATION

This application claims the benefit of U.S. Provisional Application No.60/031,755, filed Nov. 25, 1996.

FIELD OF THE INVENTION

This invention relates to perfluoroelastomer compositions which haveexcellent processability, and which, when cured, have outstandingthermal stability and chemical resistance.

BACKGROUND OF THE INVENTION

Perfluoroelastomers (elastomeric perfluoropolymers) are polymericmaterials which exhibit outstanding high temperature tolerance andchemical resistance. Consequently, such compositions are particularlyadapted for use as seals and gaskets in systems in which elevatedtemperatures and/or corrosive chemicals are encountered. The outstandingproperties of perfluoropolymers are largely attributable to thestability and inertness of the copolymerized perfluorinated monomerunits which make up the major portion of the polymer backbone, e.g.,tetrafluoroethylene and perfluoro(alkyl vinyl) ethers. In order tocompletely develop elastomeric properties, perfluoropolymers aretypically crosslinked, i.e. vulcanized. To this end, a small percentageof cure site monomer is copolymerized with the perfluorinated monomerunits. Cure site monomers containing at least one nitrile group, forexample perfluoro-8-cyano-5-methyl-3,6-dioxa-1-octene, are especiallypreferred. Such compositions are described in U.S. Pat. No. 4,281,092and 4,394,489; and in International Application WO 95/22575.

A recently-developed class of perfluoroelastomers havingcarbonyl-containing functional groups is disclosed in co-pending U.S.patent application Ser. No. 08/755,919, entitled "Fast-curingPerfluoroelastomer Compositions," filed Nov. 25, 1996. These polymersare characterized by having carbonyl-containing functional groups,including carboxyl groups, carboxylate groups, carboxamide groups, andmixtures thereof. Preferably, the carbonyl-containing functional groupsare generated as a result of persulfate initiation of the polymerizationreaction and the reaction is carried out in the absence of sulfite orbisulfite reducing agents. The carbonyl-containing perfluoroelastomersexhibit outstanding cure characteristics but they are difficult toprocess in certain end-uses because of their relatively high viscosity.A method for decreasing viscosity of the carbonyl-containingperfluoroelastomers is disclosed in co-pending U.S. patent applicationSer. No. 08/755,946, entitled "Perfluoroelastomer Composition HavingImproved Processability", filed Nov. 25, 1996 now abandoned. Theresultant lower viscosity perfluoroelastomers are suitable for use in awide variety of end-use applications and process easily.

It would also be desirable to have low viscosity analogues of othertypes of perfluoroelastomers, for example those containing mixedsulfonate/carboxylate end groups.

SUMMARY OF THE INVENTION

This invention is directed to a process for preparation of an uncuredperfluoroelastomer composition comprising the steps of

A) preparing a perfluoroelastomer having a plurality ofcarbonyl-containing functional groups selected from the group consistingof carboxyl endgroups, carboxylate endgroups, carboxamide endgroups, andmixtures thereof by copolymerizing a monomer mixture comprising

a) a perfluoroolefin monomer, b) a perfluorovinyl ether monomer selectedfrom the group consisting of perfluoro(alkyl vinyl) ethers,perfluoro(alkoxy vinyl) ethers, and mixtures thereof, and (c) a curesite monomer at a pressure of from 4-10 MPa, in the presence of apersulfate free radical initiator, wherein

i) the feed ratio of monomer to initiator is controlled so that theratio of the radical flux to the polymerization rate, Ri/Rp, is fromabout 10 to 50 millimoles per kilogram, and ii) no more than 20 molepercent of a reducing agent is present in the polymerization mixture,wherein the reducing agent is selected from the group consisting ofsulfite and bisulfite reducing agents, and the mole percentage ofreducing agent is based on the total moles of persulfate free radicalinitiator and reducing agent present in the polymerization mixture;

B) isolating said perfluoroelastomer having a plurality ofcarbonyl-containing functional groups and sulfonyl-containing functionalgroups; and

C) heating said isolated perfluoroelastomer having a plurality ofcarbonyl-containing functional groups and sulfonyl-containing functionalgroups at a temperature of at least 230° C. for a time sufficient to atleast partially decarboxylate the perfluoroelastomer.

In addition, the present invention is directed to an uncuredperfluoroelastomer composition prepared by a process comprising thesteps of

A) preparing a perfluoroelastomer having a plurality ofcarbonyl-containing functional groups selected from the group consistingof carboxyl end groups, carboxylate endgroups, carboxamide endgroups,and mixtures thereof by copolymerizing a monomer mixture comprising a) aperfluoroolefin monomer, b) a perfluorovinyl ether monomer selected fromthe group consisting of perfluoro(alkyl vinyl) ethers, perfluoro(alkoxyvinyl) ethers, and mixtures thereof, and c) a cure site monomer at apressure of from 4-10 MPa, in the presence of a persulfate free radicalinitiator, wherein

i) the feed ratio of monomer to initiator is controlled so that theratio of the radical flux to the polymerization rate, Ri/Rp, is fromabout 10 to 50 millimoles per kilogram, and ii) no more than 20 molepercent of a reducing agent is present in the polymerization mixture,wherein the reducing agent is selected from the group consisting ofsulfite and bisulfite reducing agents, and the mole percentage ofreducing agent is based on the total moles of persulfate free radicalinitiator and reducing agent present in the polymerization mixture;

B) isolating said perfluoroelastomer having a plurality ofcarbonyl-containing functional groups and sulfonyl-containing functionalgroups; and

C) heating said isolated perfluoroelastomer having a plurality ofcarbonyl-containing functional groups and sulfonyl-containing functionalgroups at a temperature of at least 230° C. for a time sufficient to atleast partially decarboxylate the perfluoroelastomer.

The invention is further directed to curable compositions comprising theproduct produced by the above-described process and a curing agent.

DETAILED DESCRIPTION OF THE INVENTION

The perfluoroelastomers of the present invention comprise a class ofperfluoroelastomers wherein ionized or ionizable sulfonyl-containingendgroups are present, and ionized or ionizable carbonyl-containingendgroups are also generally present. By ionized or ionizablesulfonyl-containing endgroups is meant sulfonate endgroups and sulfonicacid endgroups, respectively. By ionized or ionizablecarbonyl-containing endgroups is meant carboxylate endgroups orcarboxylic acid endgroups, respectively. Preferably, no more than 50% ofthe endgroups will be represented by sulfonic acid or sulfonateendgroups because higher levels of such endgroups are detrimental topolymer processability.

The present invention also includes curable compositions comprising theabove-described two types of perfluoroelastomers in combination withcuratives.

Perfluoroelastomers are polymeric compositions having copolymerizedunits of at least two principal perfluorinated monomers. Generally, oneof the principal comonomers is a perfluoroolefin while the other is aperfluorovinyl ether. Representative perfluorinated olefins includetetrafluoroethylene and hexafluoropropylene. Suitable perfluorinatedvinyl ethers are those of the formula

    CF.sub.2 ═CFO(R.sub.f' O).sub.n (R.sub.f" O).sub.m R.sub.f(I)

where R_(f') and R_(f") are different linear or branchedperfluoroalkylene groups of 2-6 carbon atoms, m and n are independently0-10, and R_(f) is a perfluoroalkyl group of 1-6 carbon atoms.

A preferred class of perfluoro(alkyl vinyl) ethers includes compositionsof the formula

    CF.sub.2 ═CFO(CF.sub.2 CFXO).sub.n R.sub.f             (II)

where X is F or CF₃, n is 0-5, and R_(f) is a perfluoroalkyl group of1-6 carbon atoms.

Most preferred perfluoro(alkyl vinyl) ethers are those wherein n is 0 or1 and R_(f) contains 1-3 carbon atoms. Examples of such perfluorinatedethers include perfluoro(methyl vinyl) ether and perfluoro(propyl vinyl)ether. Other useful monomers include compounds of the formula

    CF.sub.2 ═CFO (CF.sub.2).sub.m CF.sub.2 CFZO!.sub.n R.sub.f(III)

where R_(f) is a perfluoroalkyl group having 1-6 carbon atoms, m=0 or 1,n=0-5, and Z═F or CF₃.

Preferred members of this class are those in which R_(f) is C₃ F₇, m=0,and n=1. Additional perfluoro(alkyl vinyl) ether monomers includecompounds of the formula

    CF.sub.2 ═CFO (CF.sub.2 CFCF.sub.3 O).sub.n (CF.sub.2 CF.sub.2 CF.sub.2 O).sub.m (CF.sub.2).sub.p !C.sub.x F.sub.2x+1             (IV)

where m and n=1-10, p=0-3, and x=1-5.

Preferred members of this class include compounds where n=0-1, m=0-1,and x=1.

Examples of useful perfluoro(alkoxy vinyl) ethers include

    CF.sub.2 ═CFOCF.sub.2 CF(CF.sub.3)O(CF.sub.2 O).sub.m C.sub.n F.sub.2n+1(V)

where n=1-5, m=1-3, and where, preferably, n=1.

Mixtures of perfluoro(alkyl vinyl) ethers and perfluoro(alkoxy vinyl)ethers may also be used.

Preferred copolymers are composed of tetrafluoroethylene and at leastone perfluoro(alkyl vinyl) ether as principal monomer units. In suchcopolymers, the copolymerized perfluorinated ether units constitute fromabout 15-50 mole percent of total monomer units in the polymer.

The perfluoropolymer further contains copolymerized units of at leastone cure site monomer, generally in amounts of from 0.1-5 mole percent.The range is preferably between 0.4-1.5 mole percent. Although more thanone type of cure site monomer may be present, most commonly one curesite monomer is used and it contains at least one nitrile substituentgroup. Suitable cure site monomers include nitrile-containingfluorinated olefins and nitrile-containing fluorinated vinyl ethers.Useful nitrile-containing cure site monomers include those of theformulas shown below.

    CF.sub.2 ═CF--O(CF.sub.2).sub.n --CN                   (VI)

where n=2-12, preferably 2-6;

    CF.sub.2 ═CF--O CF.sub.2 --CF.sub.1 CF.sub.3 --O!.sub.n --CF.sub.2 --CFCF.sub.3 --CN                                         (VII)

where n=0-4, preferably 0-2; and

    CF.sub.2 ═CF-- OCF.sub.2 CFCF.sub.3 !.sub.x --O--(CF.sub.2).sub.n --CN(VIII)

where x=1-2, and n=1-4.

Those of formula (VIII) are preferred. Especially preferred cure sitemonomers are perfluorinated polyethers having a nitrile group and atrifluorovinyl ether group. A most preferred cure site monomer is

    CF.sub.2 ═CF OCF.sub.2 CF(CF.sub.3)!OCF.sub.2 CF.sub.2 CN(IX)

i.e. perfluoro(8-cyano-5-methyl-3,6-dioxa-1-octene) or 8-CNVE.

Other cure site monomers include olefins represented by the formula R₁CH═CR₂ R₃, wherein R₁ and R₂ are independently selected from hydrogenand fluorine and R₃ is independently selected from hydrogen, fluorine,alkyl, and perfluoroalkyl. The perfluoroalkyl group may contain up toabout 12 carbon atoms. However, perfluoroalkyl groups of up to 4 carbonatoms are preferred. In addition, the cure site monomer preferably hasno more than three hydrogen atoms. Examples of such olefins includeethylene, vinylidene fluoride, vinyl fluoride, trifluoroethylene,1-hydropentafluoropropene, and 2-hydropentafluoropropene as well asbrominated olefins such as 4-bromotetrafluorobutene-1 andbromotrifluoroethylene.

An especially preferred perfluoroelastomer contains 53.0-79.9 molepercent tetrafluoroethylene, 20.0-46.9 mole percent perfluoro(methylvinyl) ether and 0.4 to 1.5 mole percent nitrile-containing cure sitemonomer.

Any carbonyl-containing functional groups present in theperfluoroelastomers of this invention are either present as polymerendgroups or as pendant functionalities introduced as a result ofcopolymerization of fluorinated carbonyl-containing comonomers. Forpurposes of this invention carbonyl-containing endgroups are carboxylicacid endgroups, carboxylic acid salt endgroups, or carboxamide (i.e.amides of carboxylic acids) endgroups. By carbonyl-containing comonomeris meant a fluorinated monomer having a copolymerizable double bond andat least one pendant carboxylic acid group (including salts thereof),pendant carboxylic acid ester group, or pendant carboxamide group. Suchcomonomers are represented by compounds represented by formulas (X) and(XI):

    CF.sub.2 ═CFO(CF.sub.2).sub.n X                        (X)

    CF.sub.2 ═CFO CF.sub.2 CF(CF.sub.3)O!.sub.n (CF.sub.2).sub.x X(XI)

where n=1-4,

x=2-5, and

X=CO₂ H, CO₂ ⁻, CONH₂, or CO₂ CH₃

Depending on the carbonyl-containing comonomer selected, the resultingpolymer would have carboxyl, carboxylate, or carboxamide (i.e.carboxylic acid amide) groups at any point on the chain, i.e. at thechain end, within the chain, or both.

Perfluoroelastomers having carboxyl or carboxylate endgroups can beprepared by polymerization of mixtures of perfluoroolefins andperfluorovinyl ethers in the presence of a free radical generatinginitiator either in bulk, in solution in an inert solvent, in aqueoussuspension, or in aqueous emulsion. Perfluoroelastomer polymerizationtechniques are described in general in Logothetis, Prog. Polymn. Sci,Vol. 14, 252-296 (1989) and in U.S. Pat. No. 5,677,389. The Logothetisarticle discloses, among others, a method of polymerization involvinginitiation by persulfates, such as ammonium or potassium persulfate, inthe absence of a reducing agent. Thermally initiated free-radicalpolymerization using persulfates in the absence of a reducing agentresults in the production of polymers having carboxylic acid end groupswhich ionize to form carboxylate groups. Reducing agents include suchcompounds as sodium sulfite and sodium hydrogen sulfite.

If reducing agents are additionally present in the polymerizationmixture, then perfluoroelastomers will be produced which contain amixture of carboxylate, carboxylic acid, sulfonate, and sulfonic acidend groups. If the concentration of reducing agent present is more than20 mole percent, based on the total number of moles of reducing agentand persulfate initiator present in the polymerization mixture, thenprocessability of the isolated polymer is adversely affected. Thepresence of ionized or ionizable endgroups has detrimental effects onpolymer processability, i.e., it increases as bulk viscosity.Processability of perfluoroelastomers having carboxyl-containingendgroups can be improved by decarboxylation. However, even after adecarboxylation step, those polymers prepared in the presence of greaterthan 20 mole percent reducing agent, based on the total of reducingagent and initiator, have relatively high viscosities and areconsequently difficult to mill.

In order to produce the perfluoroelastomers of the present inventionwhich are either free of carboxyl-containing endgroups or which havereduced amounts of such groups, decarboxylation of carboxylatedperfluoroelastomers, such as those described above, is convenientlycarried out by heat-treating the solid carboxylated perfluoroelastomers,which have been isolated and oven-dried. It is not necessary that thepolymer be completely dry. That is, the polymer may be completely orpartially dried prior to the decarboxylation process. In order to effectdecarboxylation, the perfluoropolymer is heated to a temperaturesufficiently high, and for a sufficiently long period of time, todecarboxylate all of the endgroups and convert them to non-ionizablesubstituents, for example, difluoromethyl groups or trifluorovinylgroups. This results in a lowering of polymer viscosity. Partiallydecarboxylated perfluoroelastomers are also useful compositions and maybe prepared by heat treating the carboxylated perfluoroelastomer forshorter periods of time. Generally, a temperature of 230° C.-325° C. fora period of several minutes is sufficient to partially decarboxylate thepolymer. Thus, a circulating air oven treatment of polymer crumb orsheet at temperatures of about 230° C.-325° C. is effective in removinga fraction or substantially all of the carbonyl-containing functionalgroups. Preferably, the polymer will be heated for 30 minutes at atemperature of 280° C.-320° C. If the temperature is below 250°, thendecarboxylation may be too slow to be a commercially useful process.However, if potassium salts are used in the polymerization mixture, thenthe decarboxylation temperature can be lowered to 230° without reducingthe rate of decarboxylation to a level which is commerciallyunacceptable. For example, the initiator may be potassium persulfate,and potassium salts may be used as buffers and surfactants. A suitablebuffer is potassium dihydrogen phosphate and a suitable surfactant ispotassium perfluorooctanoate. It is desirable to decarboxylate at thelower end of the temperature range to minimize any possibility ofdegradation of copolymerized cure site monomers. If the temperature isbelow 230° C., then decarboxylation is extremely slow. If thetemperature is above 325° C., then the amount of cure site monomer inthe polymer may be reduced by the heat treatment. At the lowesttemperatures, the required heating time is much longer than at thehighest temperatures and typical heating times range from about 5minutes to about 24 hours. The decarboxylation can also be performed ina heated extruder, in a compression mold, or any other conventionalheated elastomer processing equipment. The appropriate time will dependon the degree of decarboxylation desired. It is readily understood bythose skilled in the art that other means of increasing the internaltemperature of the polymer may be used, for example exposure tomicrowave radiation.

Unexpectedly, the perfluoroelastomers are not degraded by the heattreating process and retain their excellent response to vulcanizationwith a variety of curing agents. For example, it has been found that ifcopolymerized units of nitrile-containing cure site monomers, e.g.8-CNVE, are present in the perfluoroelastomer, their concentration isessentially unaffected by a properly chosen heating cycle.

The decarboxylation process results in production of perfluoroelastomershaving sulfonyl-containing endgroups and a reduced level ofcarboxyl-containing endgroups. The polymers have significantly loweredbulk viscosity compared to the non-decarboxylated polymers, thusimproving processability. Another advantage of the lower bulk viscosityof the decarboxylated polymers is that decarboxylated polymers of highermolecular weight than would have been processable in thenon-decarboxylated form can now be used commercially. These highermolecular weight polymers impart improved physical properties (e.g.tensile strength, compression set and reduced weight loss at hightemperatures) to finished articles. The viscosity decrease is related tothe reduction of ionic difunctionality which results from the heattreatment. Mooney viscosity, ML-10@121° C. decreases of at least 5% aretypical upon complete decarboxylation.

Low viscosity perfluoroelastomer compositions may also be prepared byblending appropriate amounts of the decarboxylated and partiallydecarboxylated perfluoroelastomer compositions of the invention with asecond perfluoroelastomer. The second perfluoroelastomer may haveionized or ionizable end groups, or it may be a perfluoroelastomerhaving bromine-containing groups or iodine-containing groups. Theperfluoroelastomer blend compositions will exhibit physical propertiestypical of the perfluoroelastomer components. In addition, they will becharacterized by enhanced processability, for example extrusion behaviorand mixing properties.

The carbonyl content of the perfluoroelastomers of the invention may bedetermined by an integrated absorbance ratio method based on Fouriertransform infrared analysis. Specifically, the total content ofcarboxyl, carboxylate, and carboxamide groups in the polymer isdetermined by measuring the integrated carbonyl absorbance (i.e. thetotal area of all peaks in the region 1620-1840 cm⁻¹) of thin polymerfilms using a Fourier transform IR spectrometer. In order to compare thecarbonyl level in different polymer samples, integrated absorbance isnormalized for differences in polymer film thickness by taking the ratioof the carbonyl integrated absorbance to the thickness band integratedabsorbance. Thickness band integrated absorbance is the total area ofall peaks in the region 2200-2740 cm⁻¹. The integrated absorbance ofpeaks in the latter region is proportional to the thickness of thepolymer film. The integrated absorbance ratio can be readily used tocalculate the concentration of carbonyl groups in the polymer bycomparing the integrated absorbance ratio of the polymer to that of astandard polymer of known carboxyl or carboxylate content. Suchstandards may be prepared from polymers of this invention which havebeen heated in order to completely decarboxylate them, as described inco-pending U.S. patent application Ser. No. 08/755,919, entitled"Fast-curing Perfluoroelastomer Composition," filed Nov. 25, 1996. Inthe case where a carbonyl-containing cure site monomer is present in thepolymer chain, the integrated absorbance due to the carbonyl group issubtracted from the total integrated absorbance in order to determinethe concentration of the carbonyl-containing endgroups. Known amounts ofa carbonyl-containing compound such as ammonium perfluorooctanoate maythen be added to the substantially completely decarboxylated polymer inorder to produce a calibration curve of integrated absorbance ratioversus concentration of ammonium perfluorooctanoate.

Perfluoroelastomer compositions of this invention also comprisecompositions in which polymer plus curing agent is present. Generally,when used commercially, perfluoroelastomer compositions will be composedof a polymeric component, a curing agent, and optional additives. Thepolymeric component is a perfluoroelastomer of the types describedabove.

When the perfluoroelastomer has copolymerized units of anitrile-containing cure site monomer, and the polymer is substantiallyfree of carbonyl-containing functional groups, a cure system based on anorganotin compound can be utilized. Suitable organotin compounds includeallyl-, propargyl-, triphenyl- and allenyl tin curatives. Tetraalkyltincompounds or tetraaryltin compounds are the preferred curing agents foruse in conjunction with nitrile-substituted cure sites. The amount ofcuring agent employed will necessarily depend on the degree ofcrosslinking desired in the final product as well as the type andconcentration of reactive moieties in the perfluoroelastomer. Ingeneral, about 0.5-10 phr of curing agent can be used, and 1-4 phr issatisfactory for most purposes. It is believed that the nitrile groupstrimerize to form s-triazine rings in the presence of curing agents suchas organotin, thereby crosslinking the perfluoroelastomer. Thecrosslinks are thermally stable, even at temperatures of 275° C. andabove. It has been found that the decarboxylated orpartially-decarboxylated perfluoroelastomers have an unacceptably slowcure rate when compounded in accordance with conventional organotincurative recipes unless an accelerator is added. In particular, it hasbeen found that organic or inorganic ammonium salts are unusuallyeffective accelerators. Preferred accelerators include ammoniumperfluorooctanoate, ammonium perfluoroacetate, ammonium thiocyanate, andammonium sulfamate. These accelerators are disclosed in U.S. Pat. No.5,677,389, and are generally used in quantities of 0.1-2.0 parts perhundred parts perfluoroelastomer, preferably in quantities of 0.5-1.0parts per hundred parts perfluoroelastomer. In addition, ammonium saltsof organic and inorganic acids may be used as curing agents. Suitableammonium salts and quantities effective for curing perfluoroelastomersare disclosed in U.S. Pat. No. 5,565,512. Fast-curing perfluoroelastomercompositions wherein the perfluoroelastomer component has a plurality ofcarbonyl-containing functional groups and the curative is an organotincurative are disclosed in co-pending U.S. patent application Ser. No.08/755,919, entitled "Fast-curing Perfluoroelastomer Compositions,"filed Nov. 25, 1996.

A preferred cure system, useful for perfluoroelastomers containingnitrile-containing cure sites utilizes bis(aminophenols) of the formulas##STR1## and tetraamines of the formula ##STR2## where A is SO₂, O, CO,alkyl of 1-6 carbon atoms, perfluoroalkyl of 1-10 carbon atoms, or acarbon-carbon bond linking the two aromatic rings. The amino andhydroxyl groups in formulas XII and XIII above, are interchangeably inthe meta and para positions with respect to the group A. Preferably, thecuring agent is a compound selected from the group consisting of 4,4'-2,2,2-trifluoro-1-(trifluoromethyl)-ethylidene!bis(2-aminophenol);4,4'-sulfonylbis(2-aminophenol); 3,3'-diaminobenzidine; and3,3',4,4'-tetraaminobenzophenone. The first of these is the mostpreferred and will be referred to as bis(aminophenol) AF. The curingagents can be prepared as disclosed in U.S. Pat. No. 3,332,907 toAngelo. Bis(aminophenol) AF can be prepared by nitration of 4,4'-2,2,2-trifluoro-1-(trifluoromethyl) ethylidene!bisphenol (i.e. bisphenolAF), preferably with potassium nitrate and trifluoroacetic acid,followed by catalytic hydrogenation, preferably with ethanol as asolvent and a catalytic amount of palladium on carbon as catalyst. Thelevel of curing agent should be chosen to optimize the desiredproperties of the vulcanizate. In general, a slight excess of curingagent over the amount required to react with all the cure sites presentin the polymer is used. Typically, 0.5-5.0 parts by weight of thecurative per 100 parts of polymer is required. The preferred range is1.0-2.0 parts.

Peroxides may also be utilized as curing agents. Useful peroxides arethose which generate free radicals at curing temperatures. A dialkylperoxide which decomposes at a temperature above 50° C. is especiallypreferred. In many cases it is preferred to use a di-tertiarybutylperoxide having a tertiary carbon atom attached to peroxy oxygen. Amongthe most useful peroxides of this type are2,5-dimethyl-2,5-di(tertiarybutylperoxy)hexyne-3 and2,5-dimethyl-2,5-di(tertiarybutylperoxy)hexane. Other peroxides can beselected from such compounds as dicumyl peroxide, dibenzoyl peroxide,tertiarybutyl perbenzoate, and di1,3-dimethyl-3-(t-butylperoxy)-butyl!carbonate. Generally, about 1-3parts of peroxide per 100 parts of perfluoroelastomer is used. Anothermaterial which is usually blended with the composition as a part of thecurative system is a coagent composed of a polyunsaturated compoundwhich is capable of cooperating with the peroxide to provide a usefulcure. These coagents can be added in an amount equal to 0.1 and 10 partsper hundred parts perfluoroelastomer, preferably between 2-5 parts perhundred parts perfluoroelastomer. The coagent may be one or more of thefollowing compounds: triallyl cyanurate; triallyl isocyanurate;tri(methylallyl isocyanurate; tris(diallylamine)-s-triazine; triallylphosphite; N,N-diallyl acrylamide; hexaallyl phosphoramide;N,N,N',N'-tetraalkyl tetraphthalamide; N,N,N',N'-tetraallyl malonamide;trivinyl isocyanurate; 2,4,6-trivinyl methyltrisiloxane; andtri(5-norbomene-2-methylene)cyanurate. Particularly useful is triallylisocyanurate.

Depending on the cure site monomers present, it is also possible to usea dual cure system. For example, perfluoroelastomers havingcopolymerized units of nitrile-containing cure site monomers can becured using a curative comprising a mixture of a peroxide in combinationwith an organotin curative and a coagent. Generally, 0.3-5 parts ofperoxide, 0.3-5 parts of coagent, and 0.1-10 parts of organotin curativeare utilized.

Additives, such as carbon black, stabilizers, plasticizers, lubricants,fillers, and processing aids typically utilized in perfluoroelastomercompounding can be incorporated into the compositions of the presentinvention, provided they have adequate stability for the intendedservice conditions. In particular, low temperature performance can beenhanced by incorporation of perfluoropolyethers.

Carbon black fillers are used in elastomers as a means to balancemodulus, tensile strength, elongation, hardness, abrasion resistance,conductivity, and processability of the compositions. Inperfluoroelastomer compositions, small particle size, high surface areacarbon blacks have been the fillers of choice. A grade commonly chosenis SAF carbon black, a highly reinforcing black with typical averageparticle size of about 14 nm and designated N 110 in Group No. 1,according to ASTM D-1765. The particular carbon blacks useful in thecompositions of the present invention are those described in WO95/22575. These particular carbon blacks have average particle sizes ofat least about 100 nm to about 500 nm as determined by ASTM D-3849.Examples include MT blacks (medium thermal black) designated N-991,N-990, N-908, and N-907, and large particle size furnace blacks. MTblacks are preferred. When used, 1-70 phr of large size particle blackis generally sufficient, and this amount does not retard cure time.

In addition, fluoropolymer fillers may also be present in thecomposition. Generally from 1 to 50 parts per hundred perfluoroelastomerof a fluoropolymer filler is used, and preferably at least about 5 partsper hundred parts perfluoroelastomer is present. The fluoropolymerfiller can be any finely divided, easily dispersed plastic fluoropolymerthat is solid at the highest temperature utilized in fabrication andcuring of the perfluoroelastomer composition. By solid, it is meant thatthe fluoroplastic, if partially crystalline, will have a crystallinemelting temperature above the processing temperature(s) of theperfluoroelastomer(s). Such finely divided, easily dispersedfluoroplastics are commonly called micropowders or fluoroadditives.Micropowders are ordinarily partially crystalline polymers.

Micropowders that can be used in the composition of the inventioninclude, but are not limited to, those based on the group of polymersknown as tetrafluoroethylene (TFE) polymers. This group includeshomopolymers of TFE (PTFE) and copolymers of TFE with such smallconcentrations of at least one copolymerizable modifying monomer thatthe resins remain non-melt-fabricable (modified PTFE). The modifyingmonomer can be, for example, hexafluoropropylene (HFP), perfluoro(propylvinyl) ether (PPVE), perfluorobutylethylene, chlorotrifluoroethylene, oranother monomer that introduces side groups into the polymer molecule.The concentration of such copolymerized modifiers in the polymer isusually less than 1 mole percent. The PTFE and modified PTFE resins thatcan be used in this invention include both those derived from suspensionpolymerization and from emulsion polymerization.

High molecular weight PTFE used in production of micropowder is usuallysubjected to ionizing radiation to reduce molecular weight. Thisfacilitates grinding and enhances friability if the PTFE is produced bythe suspension polymerization process, or suppresses fibrillation andenhances deagglomeration if the PTFE is produced by the emulsionpolymerization process. It is also possible to polymerize TFE directlyto PTFE micropowder by appropriate control of molecular weight in theemulsion polymerization process, such as disclosed by Kuhls et al. inU.S. Pat. No. 3,956,000. Morgan, in U.S. Pat. No. 4,879,362, discloses anon-melt-fabricable, non-fibrillating modified PTFE produced by theemulsion (dispersion) polymerization process. This polymer formsplatelets on shear blending into elastomeric compositions, instead offibrillating.

TFE polymers also include melt-fabricable copolymers of TFE havingsufficient concentrations of copolymerized units of one or more monomersto reduce the melting point significantly below that of PTFE. Suchcopolymers generally have melt viscosity in the range of 0.5-60×10³Pa.s, but viscosities outside this range are known. Perfluoroolefins andperfluoro(alkyl vinyl) ethers are preferred comonomers.Hexafluoropropylene and perfluoro(propyl vinyl) ether are mostpreferred. Melt fabricable TTE copolymers such as FEP(TFE/hexafluoropropylene copolymer) and PFA TFE/perfluoro(propylvinyl)ether copolymer! can be used, provided they satisfy constraints onmelting temperature with respect to perfluoroelastomer processingtemperature. These copolymers can be utilized in powder form as isolatedfrom the polymerization medium, if particle size is acceptable, or theycan be ground to suitable particle size starting with stock of largerdimensions.

The curable compositions of the present invention are useful inproduction of gaskets, tubing, and seals. Such articles are produced bymolding a compounded formulation of the curable composition with variousadditives under pressure, curing the part, and then subjecting it to apost cure cycle. The cured compositions have excellent thermal stabilityand chemical resistance. They are particularly useful in applicationssuch as seals and gaskets for manufacturing semiconductor devices, andin seals for high temperature automotive uses.

EXAMPLE

To a 5575 ml, stirred, water-jacketed, stainless steel autoclaveoperated continuously at a temperature of 70° C. and a pressure of 4.1MPa, is fed tetrafluoroethylene (TFE) and perfluoro(methyl vinyl) ether(PMVE) at the rates of 333 g/hour and 386 g/hour, respectively, using adiaphragm compressor. Perfluoro-(8-cyano-5-methyl-3,6-dioxa-1-octene)(8CNVE) is also fed at the rate of 21.1 g/hour. Each of two aqueoussolutions is fed separately at the rate of 688 ml/hour. One of thesesolutions consists of 287 g of ammonium persulfate, 200 g disodiumhydrogen phosphate, and 272 g ammonium perfluorooctanoate in 20 litersof deaerated, de-ionized water. The second solution consists of 39.6 gsodium sulfite, and 272 g ammonium perfluorooctanoate in 20 litersdeaerated, de-ionized water. Polymer latex is removed continuouslythrough a let-down valve and unreacted monomers are vented. The latex iscoagulated by adding 9.5 liters latex, at ambient temperature, to 37.85liters stirred, de-ionized water at 85° C., re-equilibrating the mixtureat 85° C., and adding 3 liters of a solution of 50 g magnesium sulfateheptahydrate per liter of de-ionized water. The resulting slurry isstirred for one hour at 85° C., filtered, and then dried at 80° C. in aforced air oven for at least eighteen hours. The yield of polymer isapproximately 350 g per liter of latex. The composition of the polymeris approximately 43 wt.% PMVE, 2.1 wt.% 8CNVE, and 54.9 wt.% TFE. Thepolymer is decarboxylated by heating in an air oven at 300° C. for onehour, thereby reducing the Mooney viscosity, ML-10@121° C.

I claim:
 1. A process for preparation of an uncured perfluoroelastomercomposition comprising the steps ofA) preparing a perfluoroelastomerhaving a plurality of carbonyl-containing functional groups selectedfrom the group consisting of carboxyl endgroups, carboxylate endgroups,carboxamide endgroups, and mixtures thereof by copolymerizing a monomermixture comprising a) a perfluoroolefin monomer, b) a perfluorovinylether monomer selected from the group consisting of perfluoro(alkylvinyl) ethers, perfluoro(alkoxy vinyl) ethers, and mixtures thereof, andc) a cure site monomer at a pressure of from 4-10 MPa, in the presenceof a persulfate free radical initiator, wherein i) the feed ratio ofmonomer to initiator is controlled so that the ratio of the radical fluxto the polymerization rate, Ri/Rp, is from about 10 to 50 millimoles perkilogram, and ii) no more than 20 mole percent of a reducing agent ispresent in the polymerization mixture, wherein the reducing agent isselected from the group consisting of sulfite and bisulfite reducingagents, and the mole percentage of reducing agent is based on the totalmoles of persulfate free radical initiator and reducing agent present inthe polymerization mixture; B) isolating said perfluoroelastomer havinga plurality of carbonyl-containing functional groups andsulfonyl-containing functional groups; and C) heating said isolatedperfluoroelastomer having a plurality of carbonyl-containing functionalgroups and sulfonyl-containing functional groups at a temperature of atleast 230° C. for a time sufficient to at least partially decarboxylatethe perfluoroelastomer.
 2. A process of claim 1 wherein the heating instep C) takes place at a temperature within the range of 280° C.-320° C.3. A process of claim 1 wherein step C) is accomplished by heating in anoven.
 4. A process of claim 1 wherein step C) is accomplished by heatingin an extruder.
 5. A process of claim 1 wherein step C) is accomplishedby heating in a compression mold.
 6. A process of claim 1 wherein stepC) is accomplished by heating using microwave radiation.
 7. A process ofclaim 1 wherein the persulfate free radical initiator is potassiumpersulfate.
 8. A process of claim 1 wherein the persulfate free radicalinitiator is ammonium persulfate.